Membrane module system with bundle enclosures and pulsed aeration and method of operation

1. A method of operating a membrane filter module having hollow fiber membranes arranged in a substantially vertical orientation, that are immersed in a liquid in a tank, the method comprising:

operating the module submerged in the liquid wherein the module includes:

a header;

a bundle containing a plurality of hollow fiber membranes, wherein a lower end of each hollow fiber membrane is fixed in the header;

a gasification device adapted to periodically generate a gaseous bubble and configured to release the gaseous bubble within the bundle, wherein the gaseous bubble travels through an air tube that starts from the gasification device and goes into the header; and

an enclosure that substantially surrounds the bundle that extends from a lower region to an upper region of the membrane bundle, wherein the enclosure is configured to retain the liquid introduced into the enclosure such that the liquid surrounds the membrane bundle;

applying a pressure that is less than an ambient pressure of the tank to a permeate collection chamber, that is in fluid communication with the hollow fiber membranes, wherein applying the pressure is configured to cause a portion of the liquid to pass through the hollow fiber membranes as permeate into the permeate collection chamber;

supplying a gas stream to the gasification device;

wherein the gaseous bubble has a cross-sectional area that corresponds with a cross-sectional area of the enclosure, such that the cross-sectional area of the gaseous bubble occupies substantially the entire cross-sectional area of the enclosure as it flows along the bundle.

2. The method of claim 1 , further includes controlling the gas stream such that the gasification device generates the gaseous bubble at a rate of between 2 and 70 bubbles per minute.

3. The method of claim 1 , further includes controlling the gas stream such that the gasification device generates the gaseous bubble at substantially regular intervals.

4. The method of claim 1 , wherein the gaseous bubble has a cross-sectional area that ranges from about 10 in 2 to about 14 in 2 .

5. The method of claim 1 , wherein the enclosure has an internal cross-sectional area that ranges from about 10 in 2 to about 14 in 2 .

6. The method of claim 1 , further includes supplying the gas stream to a plurality of gasification devices, wherein each gasification devices is associated with a bundle.

7. The method of claim 1 , wherein releasing the gaseous buddle within the bundle includes releasing the gaseous bubble from an air tube through the header into the center of the bundle.

8. The method of claim 1 , wherein releasing the gaseous bubble within the bundle includes releasing the gaseous bubble from an air tube into an expansion chamber that is within the header, wherein the expansion chamber has a greater diameter than the aeration tube, and further wherein the bubble expands in the expansion chamber before it is released into the center of the bundle.

9. The method of claim 1 , wherein the module is capable of an average fouling rate of about 0.22 mbar/min or less when operating at a flux of 30 LMH and having an aeration air flow rate of about 0.088 N/m 3 /hr per m 2 of membrane area when processing a liquid medium that has MLSS of about 12.2 g/l and a TTF of about 120 seconds and is at a temperature of about 16.5° C.

10. The method of claim 1 , wherein the module is capable of an average fouling rate of about 5.3 mbar/min or less when operating at a flux of 60 LMH and having an aeration air flow rate of about 0.088 N/m 3 /hr per m 2 of membrane area when processing a liquid medium that has MLSS of about 12.2 g/l and a TTF of about 120 seconds and is at a temperature of about 16.5° C.

11. The method of claim 1 , wherein the module is capable of an average fouling rate of about 0.09 mbar/min or less when operating at a flux of 30 LMH and having an aeration air flow rate of about 0.215 N/m 3 /hr per m 2 of membrane area when processing a liquid medium that has MLSS of about 12.2 g/l and a TTF of about 120 seconds and is at a temperature of about 16.5° C.

12. The method of claim 1 , wherein the module is capable of an average fouling rate of about 0.94 mbar/min or less when operating at a flux of 60 LMH and having an aeration air flow rate of about 0.215 N/m 3 /hr per m 2 of membrane area when processing a liquid medium that has MLSS of about 12.2 g/l and a TTF of about 120 seconds and is at a temperature of about 16.5° C.

13. The method of claim 1 , wherein a cage gap between the top of the header and the bottom of the enclosure is between about 0.5 inches and about 5 inches, and further wherein the gaseous bubble pulls in a portion of the liquid through the cage gap.

14. A method of scouring external surfaces of hollow fiber membranes arranged in a substantially vertical orientation that are immersed in a liquid in a tank, the method comprising:

operating the module submerged in the liquid wherein the module includes:

a header;

a bundle containing a plurality of hollow fiber membranes, wherein a lower end of each hollow fiber membrane is fixed in the header;

a gasification device adapted to periodically generate a gaseous bubble and configured to release the gaseous bubble within the bundle, wherein the gaseous bubble travels through an air tube that starts from the gasification device and goes into the header; and

an enclosure that substantially surrounds the bundle that extends from a lower region to an upper region of the membrane bundle, wherein the enclosure is configured to retain the liquid introduced into the enclosure such that the liquid surrounds the membrane bundle;

applying a pressure that is less than an ambient pressure of the tank to a permeate collection chamber, that is in fluid communication with the hollow fiber membranes, wherein applying the pressure is configured to cause a portion of the liquid to pass through the hollow fiber membranes as permeate into the permeate collection chamber;

supplying a gas stream to the gasification device to produce the gaseous bubble;

wherein the enclosure causes the gaseous bubble to substantially fill the cross-sectional area of the enclosure and to maintain contact with the bundle along the entire length of the bundle, thereby the gaseous bubble scours the surface of the hollow fiber membranes and removes and lifts debris from the bundle.

15. The method of claim 1 , wherein a cage gap between the top of the header and the bottom of the enclosure is between about 0.5inches and about 5 inches, and further wherein the gaseous bubble pulls in a portion of the liquid through the cage gap.

16. A method of desludging a hollow fiber membrane module, comprising:

temporarily ending a vacuum pressure applied to the module, wherein the membrane module includes:

a header;

a bundle containing a plurality of hollow-fiber membranes,

wherein a lower end of each hollow membrane is fixed in the header;

a gasification device adapted to periodically generate a gaseous bubble and configured to release the gaseous bubble within the bundle, wherein the gaseous bubble travels through an air tube that starts from the gasification device and goes into the header; and

an enclosure that substantially surrounds the bundle that extends from a lower region to an upper region of the membrane bundle, wherein the enclosure is configured to retain the liquid introduced into the enclosure such that the liquid surrounds the membrane bundle;

supplying a gas stream to the gasification device to generate a plurality of gaseous bubbles, wherein the gaseous bubbles each substantially fill the cross-sectional area of the enclosure and maintain contact with the bundle along the entire length of the bundle; and

wherein the gaseous bubbles desludge the hollow-fiber membranes by breaking apart and lifting the sludge up and out the top of the enclosure.

17. The method of claim 16 , wherein a cage gap between the top of the header and the bottom of the enclosure is between about 0.5 inches and about 5 inches, and further wherein the gaseous bubble pulls in a portion of the liquid through the cage gap.

18. The method of claim 1 , wherein the lower end of the plurality of hollow fiber membrane of the bundle extend through a plurality of holes of a fiber plate that is fixed within the header.

19. The method of claim 18 , wherein the plurality of holes of the fiber plate are divided into sections separated by channels that are configured to enable fluid and debris to travel along the bundle.

20. The method of claim 18 , wherein the fiber plate includes a center passage through which the gaseous bubble travels when released within the bundle.